JP2004330062A - Pulverizer - Google Patents

Pulverizer Download PDF

Info

Publication number
JP2004330062A
JP2004330062A JP2003128740A JP2003128740A JP2004330062A JP 2004330062 A JP2004330062 A JP 2004330062A JP 2003128740 A JP2003128740 A JP 2003128740A JP 2003128740 A JP2003128740 A JP 2003128740A JP 2004330062 A JP2004330062 A JP 2004330062A
Authority
JP
Japan
Prior art keywords
stator
rotor
circumferential direction
pulverizer
casing
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
JP2003128740A
Other languages
Japanese (ja)
Other versions
JP3832831B2 (en
Inventor
Akinori Ueno
明紀 上野
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Kawasaki Heavy Industries Ltd
Original Assignee
Kawasaki Heavy Industries Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Kawasaki Heavy Industries Ltd filed Critical Kawasaki Heavy Industries Ltd
Priority to JP2003128740A priority Critical patent/JP3832831B2/en
Publication of JP2004330062A publication Critical patent/JP2004330062A/en
Application granted granted Critical
Publication of JP3832831B2 publication Critical patent/JP3832831B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Images

Landscapes

  • Crushing And Grinding (AREA)
  • Crushing And Pulverization Processes (AREA)

Abstract

<P>PROBLEM TO BE SOLVED: To provide a pulverizer for obtaining a product with desired characteristics corresponding to the alteration of the characteristics of a raw material. <P>SOLUTION: The pulverizer comprises a short cylindrical supply casing 4 closed in one end and having a raw material supply port 3 in the circumferential wall and a cylindrical first stator 5 installed adjacently to the other end of the casing and having recessed parts and projected parts reciprocally continued circumferentially in the inner side surface. The pulverizer further comprises a cylindrical and rotation speed-variable first rotor 7 fitted in such a manner of leaving a narrow gap in the inside and having recessed parts and projected parts reciprocally continued circumferentially in the outer side surface and a cylindrical second stator 14 installed adjacently to the other end of the first stator and having recessed parts and projected parts 7a reciprocally continued circumferentially in the inner side surface. The purlverizer further comprises a cylindrical second rotor 23 fitted in such a manner of leaving a narrow gap in the inside and having recessed parts and projected parts 23a reciprocally continued circumferentially in the outer side surface and a short cylindrical discharge casing 18 closed in the other end and having a product discharge port 17 in the circumferential wall. <P>COPYRIGHT: (C)2005,JPO&NCIPI

Description

【0001】
【発明の属する技術分野】
本発明は、樹脂、トナー等の樹脂混合品、化成品、鉱物系、金属系、食品、薬品等の原料(被粉砕物)を5〜100ミクロンの微細な粒子に微粉砕する微粉砕機に関し、特に、2段ロータを有する微粉砕機に関する。
【0002】
【従来の技術】
従来、この種の微粉砕機としては、粉砕子とこれに対向する固定子とからなる第1粉砕部および回転子とこれに対向する固定子とからなる第2粉砕部の2種の粉砕部を上下垂直方向に同軸上に配し、上記第1粉砕部の回転子の外周にはこれに対向する固定子との間に一定間隙を存して放射状の粉砕子を設け、上記第2粉砕部の回転子の外周にはこれに対向する固定子との間に一定間隙を存して母線の表面に凸部を形成し、ケーシングの下部に粉砕・材料供給口を、上部に粉砕製品排出口を設けたものが開示されている(例えば、特許文献1参照)。
【0003】
【特許文献1】
特公昭59−19739号公報
【0004】
上記微粉砕機によれば、第1粉砕部にて比較的大きな塊をあらかじめ粉砕し、適当な粒子として、それを第2粉砕部にて微細に粉砕するようにしたので、回転子の耐摩耗性を著しく向上させることができる。と同時に、前もって被粉砕物を適当な粒度に粉砕しなければならないという多大の労力を省くことができる、というものである。
【0005】
又、回転軸に支持され外側表面に母線と平行な凹部と凸部を交互に周方向に連続させた回転子と、該回転子の外側に微小間隙を存して嵌装され内側表面に母線と平行な凹部と凸部を交互に周方向に連続させた固定子との間で原料を微粉砕する微粉砕機において、回転子を2段以上に区画し、原料供給口側の最下段から製品排出口側の最上段に向って凹部と凸部の数を順次増加したものも開示されている(例えば、特許文献2参照)。
【0006】
【特許文献2】
特開2000−5614号公報
【0007】
上記微粉砕機によれば、回転子と固定子の間の粉砕室に空気と共に吸引された原料は、粉砕の進展に伴って次第に粒径が小さくなり、粉砕室を出た粉砕品にはミクロンオーダーの非常に粒度分布幅の狭い粒子となり、平均粒径の著しく小さいものとなる、というものである。
【0008】
更に、回転軸に支持され外周面に母線に対し平行な凹部と凸部が交互に連続して周方向に設けられた回転子を複数段に区画すると共に下段から上段に向って順次外径を大きくし且つ凹部と凸部の数を多くし、この回転子の外側に微小間隙を存して嵌装され内周面に母線に対し平行な凹部と凸部が交互に連続して周方向に設けられた固定子を複数段に区画すると共に下段から上段に向って順次内径を大きくし且つ凹部と凸部の数を多くし、前記回転子と固定子との空間に、空気と共に吸引された原料を、前記回転子の高速回転により微粉砕するものも知られている(例えば、特許文献3参照)。
【0009】
特開2000−15123号公報
【0010】
上記微粉砕機によれば、回転子の凹凸及び固定子の凹凸の数を上段ほど多くしても、回転子の外径、固定子の内径を上段ほど大きくして、回転子と固定子との微小間隙をほぼ一定にしているので、粉砕室の断面積は減少せず、粉砕室内の流速はほぼ一定、又は、若干遅くすることが可能となり、粒子の通過時間は各部でほぼ一定、又は、粉砕室の上部ほど長くなり、粉砕処理が十分に行われる。しかも気流の圧損が小さいので、吸引送風機を大型化する必要がない。さらに、粉砕室の出口側の回転子の外径が大きいので、回転子の周速が上がり、細かくなった粒子をさらに粉砕するのに有効である、というものである。
【0011】
【発明が解決しようとする課題】
しかし、従来のいずれの微粉砕機においても、2段のロータが同一回転軸に支持されているため、各段のロータの回転数が同一となり、又、両段のロータ径を変えることによってそれぞれの周速を変えることは可能であるが、両者の周速の比率は一定に保たれる。
従って、例えば所要粒径の粉砕物(製品)を得ようとした場合、ロータの回転数が原料の特性、すなわち、被粉砕性(粉砕され易さ)や粒度により1つに特定され、この特定された回転数によって製品の粒度分布や生産量も決定されてしまう。
ところが、各段のロータの有効な周速は、原料の特性や製品の要求特性(粒度、粒度分布、粒形等)により異なり、一律ではない。
【0012】
そこで、本発明は、原料の特性の変化に対応させて所望の特性の製品を得ることが可能な微粉砕機の提供を課題とする。
【0013】
【課題を解決するための手段】
前記課題を解決するため、本発明の微粉砕機は、一端を閉止しかつ周壁に原料供給口を設けた短円筒状を呈する供給ケーシングと、供給ケーシングの他端に一端を介して連設され、内側表面に母線と平行な凹部と凸部を交互に周方向へ連続させた円筒状を呈する第1ステータと、第1ステータの内側に微小間隙を存して嵌挿され、外側表面に母線と平行な凹部と凸部を交互に周方向へ連続させた両端閉止の円筒状を呈し、回転数可変の第1ロータと、第1ステータの他端に一端を介して連設され、内側表面に母線と平行な凹部と凸部を交互に周方向へ周方向へ連続させた円筒状を呈する第2ステータと、第2ステータの内側に微小間隙を存して嵌挿され、外側表面に母線と平行な凹部と凸部を交互に周方向へ連続させた両端閉止の円筒状を呈し、回転数可変の第2ロータと、第2ステータの他端に一端を介して連設され、他端を閉止しかつ周壁に製品排出口を設けた短円筒状を呈する排出ケーシングとを備えることを特徴とする。
【0014】
一方、前記第1、第2ステータは、分離可能であることが好ましい。
前記第1、第2ロータの少なくとも一方は、可逆回転可能であることが好ましい。
前記第1、第2ロータの少なくとも一方は、反転可能であることが好ましい。
又、前記第1、第2ステータの少なくとも一方は、反転可能であることが好ましい。
【0015】
【作用】
本発明の微粉砕機においては、第1、第2ロータの回転数(周速)が個別に設定可能となる。
【0016】
第1、第2ステータ及び第1、第2ロータの配列は、垂直又は水平のいずれでもよい。
【0017】
第1ステータと第1ロータの間、及び第2ステータと第2ロータの間の微小間隙(粉砕室)は、5mm以下が好ましく、例えば、粒径5〜20μmの微粉を得る場合、1mm程度が望ましい。
第1ステータと第1ロータ間と、第2ステータと第2ロータの間の微小間隙は、同じでも異ならせてもよい。例えば、大きい粒径の原料を微粉砕する場合、第1ステータと第1ロータの間の微小間隙は、第2ステータと第2ロータの間の微小間隙より大きい方がよい。
【0018】
第1ロータと第2ロータの外径は、同じでも異ならせてもよい。例えば、粒径5〜20μmの微粉を得る場合、第2ロータの外径は、第1ロータの外径より大きくした方がよい。
【0019】
第1、第2ステータと第1、第2ロータの凹部及び凸部の横断面形状は、原料の特性や製品の要求特性により決まるが、三角形状同士、方形状同士又は三角形状と方形状の組み合わせが好ましく、それらの深さは、1〜5mm程度である。例えば、粗い(角張った)原料の場合、第1ステータと第1ロータの凹部及び凸部は、横断面三角形状同士の組み合わせの方がよい。
第1ステータ、第1ロータと第2ステータ、第2ロータの凹部及び凸部の数は、同じでも異ならせてもよい。例えば、粒径5〜20μmの微粉を得る場合、第2ステータ、第2ロータの凹部及び凸部の数は、第1ステータ、第1ロータの凹部及び凸部の数より多い方がよい。
【0020】
一方、第1ステータと第2ステータが分離可能であることにより、それぞれのステータ及びロータの清掃が可能となる。
【0021】
供給ケーシングと第1ステータ、第1ロータと回転軸等及び第2ステータと排出ケーシング、第2ロータと回転軸等もそれぞれ分離可能であることが好ましく、このようにすることにより、各部材の清掃を容易かつ確実にすることができる。
【0022】
第1、第2ロータの少なくとも一方が可逆回転可能であることにより、第1、第2ロータの回転方向が同一又は互いに逆となり、同一の場合、被粉砕物が第1ロータと第1ステータによる粉砕室から第2ロータと第2ステータによる粉砕室へ移動する際の速度変化(加速度)が小さくなる一方、互いに逆の場合、被粉砕物が第1ロータと第1ステータによる粉砕室から第2ロータと第2ステータによる粉砕室へ移動する際の速度変化が大きくなって、衝撃力が大きくなる。
又、ロータとステータの凹部及び凸部の横断面形状がそれぞれの母線に対して対称な方形状で、ロータの回転方向の違いにより粉砕性能が変化しない場合、ステータ及びロータの摩耗が均等になる。
【0023】
第1、第2ロータの少なくとも一方が反転可能であることにより、ロータとステータの凹部及び凸部の横断面形状がそれぞれの母線に対して非対称な三角形状である場合、ロータの回転方向の変更に対応可能となる。
【0024】
又、第1、第2ステータの少なくとも一方が反転可能であることにより、ロータとステータの凹部及び凸部の横断面形状がそれぞれの母線に対して非対称な三角形状である場合、ロータの回転方向の変更に対応可能となる。
【0025】
なお、供給、排出ケーシングの少なくとも一方が反転可能であることが好ましく、このようにすることにより、それぞれの原料供給口、製品排出口が接線方向に設けられている場合、ロータの回転方向の変更に対応可能となる。
【0026】
【発明の実施の形態】
以下、本発明の実施の形態について図面を参照して説明する。
図1は本発明に係る微粉砕機の実施の形態の一例を示す一部を破断した側面図である。
【0027】
図中1は後述する供給ケーシングの蓋体と位置決め部材を兼ねるべく架台2上に水平に載設した第1ベースプレートで、この第1ベースプレート1上には、周壁に原料Mを接線方向から供給するための原料供給口3を設けた両端フランジ付き短円筒状を呈し、反転(図1においては上下引っ繰り返し)可能な供給ケーシング4が、一端(図1においては下端)のフランジを当接することにより、位置決めして載置されている。
供給ケーシング4の他端(図1においては上端)には、その内径と同一外径をなす周壁の内側表面に母線と平行な凹部と凸部(図示せず)を交互に周方向へ連続させた両端フランジ付き円筒状を呈し、反転(図1においては上下引っ繰り返し)可能な第1ステータ5が、一端を供給ケーシング4の他端に嵌挿し、かつ、一端のフランジを供給ケーシング4の他端のフランジと当接することにより、同軸的に位置決めして載置されており、第1ステータ5の周壁の外側には、第1ステータ5を冷却するための冷却ジャケット6が設けられている。
第1ステータ5の内側には、外側表面に母線と平行な凹部と凸部7aを交互に周方向へ連続させた両端閉止の円筒状を呈すると共に、反転(図1においては上下引っ繰り返し)可能で、かつ、第1ステータ5とほぼ同等の長さをなす第1ロータ7が、図示しない微小間隙(粉砕室)を存して嵌挿されており、この第1ロータ7は、供給ケーシング4の軸心部に位置するようにして第1ベースプレート1に挿着した円筒状の軸受ハウジング8に軸受(図示せず)を介し支承されて挿通し、軸受ハウジング8から第1ステータ5内に突出した回転軸9の端部に、その軸心部における軸方向のほぼ中間部を介して分離可能に支持されている。
そして、回転軸9は、軸受ハウジング8から架台2側に突出した端部に設けたプーリ(図示せず)と、架台2にL形ブラケット10を介して搭載した回転数可変、かつ、可逆回転可能な第1モータ11の出力軸11aに設けたプーリ(図示せず)とにベルト12を掛け回すことにより、第1モータと連動連結されている。
【0028】
又、第1ベースプレート1上には、2本のステータ押え用ポスト(図示せず)が、供給ケーシング4の軸心を中心とする点対称位置に立設されており、両ポスト上には、第1ステータ5の他端に外嵌され、かつ、その他端のフランジに当接するほぼ円輪板状のステータ押え13が、第1ステータ5及び供給ケーシング4を第1ベースプレート1に押圧してそれらの連結部の気密性を保つべくボルト締めされている。
【0029】
前記第1ステータ5の他端には、その内径より僅かに大きな内径をなし、かつ、第1ステータ5より短い長さをなす周壁の内側表面に母線と平行な凹部と凸部(図示せず)を交互に周方向へ連続させた両端フランジ付き円筒状を呈し、反転(図1においては上下引っ繰り返し)可能な第2ステータ14が、その一端のフランジをステータ押え13と当接し、かつ、ボルト、ナット等の複数のクランプ手段15によってステータ押え13と連結されることにより、第1ステータ5に同軸的に位置決めして気密に連設されており、第2ステータ14の周壁の外側には、第1ステータ5と同様に、第2ステータ14を冷却するための冷却ジャケット16が設けられている。
第2ステータ14の他端には、その外径と同一内径をなす周壁に製品Pを接線方向へ排出する製品排出口17を設けた両端フランジ付き短円筒状を呈し、反転(図1においては上下引っ繰り返し)可能な排出ケーシング18が、一端を第2ステータ14の他端に外嵌し、かつ、一端のフランジを第2ステータ14の他端のフランジに当接することにより、同軸的に位置決めして載置されている。
なお、製品排出口17には、図示しない吸引送風機等が連ねられているものである。
排出ケーシング18の他端には、その蓋体を兼ねる第2ベースプレート19が、排出ケーシング18の他端のフランジと当接することにより、位置決めして載置されており、この第2ベースプレート19は、第2ステータ14及び排出ケーシング18を第2ベースプレート19に押圧してそれらの連結部の気密性を保つべく、ボルト、ナット等の複数の締結具20によって、第2ステータ14の他端のフランジと締結されている一方、架台2に立設した門形の分離用ポスト21の上端に水平な支軸22によって枢支され、支軸22を中心として水平な状態から垂直な状態までの約90°の角度範囲で回動可能に設けられている(図2参照)。
前記第2ステータ14の内側には、外側表面に母線と平行な凹部と凸部23aを交互に周方向へ連続させた両端閉止の円筒状を呈すると共に、反転(図1においては上下引っ繰り返し)可能で、かつ、第2ステータ14とほぼ同等の長さをなす第2ロータ23が、図示しない微小間隙(粉砕室)を存して嵌挿されており、この第2ロータ23は、排出ケーシング18の軸心部に位置するようにして第2ベースプレート19に挿着した円筒状の軸受ハウジング24に軸受(図示せず)を介し支承されて挿通し、軸受ハウジング24から第2ステータ14内に突出した回転軸(図示せず)の端部に、その軸心部における周囲方向のほぼ中間部を介して分離可能に支持されている。
そして、回転軸は、軸受ハウジング24から第2ステータ14の反対側(図1においては上方)へ突出した端部に設けたプーリ(図示せず)と、第2ベースプレート19における支軸22側にT形ブラケット25を介して搭載した回転数可変、かつ、可逆回転可能な第2モータ26の出力軸26aに設けたプーリとにベルト(共に図示せず)を掛け回わすことにより、第2モータ26と連動連結されている。
図1において27は第2モータ26を取り巻くようにしてT形ブラケット25に設けた第2ベースプレート用回り止め部材で、分離用ポスト21に設けたストッパ28と当接して第2ベースプレート19の回動を阻止するものであり、又、29は第2モータ26のプーリ、回転軸のプーリ及びベルト等を覆うカバーである。
【0030】
上記構成の微粉砕機においては、吸引送風機と第1、第2モータ11,26を作動すると、原料Mが気体と一緒に供給ケーシング4内に供給されると共に、高速回転される第1ロータ7と第1ステータ5の間の微小間隙で打撃や衝突、摩砕作用を受けて粉砕された後、更に、第1ロータ7とは別個に高速回転される第2ロータ23と第2ステータ14の間の微小間隙で打撃や衝突、摩砕、粒形調整作用を受けて微粉砕されて排出ケーシング18に至り、製品Pが気体と一緒に機外へ排出されるものである。
【0031】
上記微粉砕機において、粗い原料Mを微粉砕する場合、第1ステータ5と第1ロータ7の凹部と凸部7aは、横断面三角形状とし、第2ステータ14と第2ロータ23の凹部と凸部23aの数を第1ステータ5と第1ロータ7の凹部と凸部7aの数より大きくしたり、第2ステータ14の内径、第2ロータ23の外径を第1ステータ5の内径、第1ロータ7の外径より大きくしたり、あるいは第2ロータ23の回転数を第1ロータの回転数より多くしたりする。
又、製品Pの生産量、粒形、粒度分布の広狭等を調整する場合、原料Mの特性に対応させて第1ロータ7と第2ロータ23の回転数(周速)を適宜に組み合わせる。
更に、消費動力の少ない運転を行う場合、第1、第2ロータ7,23の回転方向を同一にする一方、より細かい製品Pを得る場合、第1、第2ロータ7,23の回転方向を互いに逆にする。
更に又、第1、第2ステータ5,14、第1、第2ロータ7,23の偏摩耗を防止するには、第1、第2ステータ5,14、第1、第2ロータ7,23及び供給、排出ケーシング4,18を適宜に反転し、かつ、第1、第2ロータ7,23を適宜に正転又は逆転させる。
【0032】
一方、原料Mの種類の変更等によって内部の清掃を行う場合には、先ず、クランプ手段15による第2ステータ14とステータ押え13の連結を解除し、図2に示すように、第2ベースプレート19を支軸22を中心として回動し、第1ステータ5と第2ステータ14を分離する。
次に、ステータ押え13による第1ステータ5及び供給ケーシング4の押圧を解除し、かつ、第1ロータ7を回転軸9から取り外すことにより、第1ステータ5、第1ロータ7及び供給ケーシング4等の個別の清掃が可能となる。
又、締結具20による第2ステータ14と第2ベースプレート19の締結を解除し、かつ、第2ロータ23を回転軸から取り外すことにより、第2ステータ14、第2ロータ23及び排出ケーシング18等の個別の清掃が可能となる。
【0033】
なお、上述した実施の形態においては、第1、第2ロータ7,23の駆動は、伝動手段を介在して第1、第2モータ11,26の回転を伝える場合について説明したが、これに限定されるものではなく、回転軸にモータのロータを直接組み込んだビルトインモータにより直接行うようにしてもよい。
又、第1、第2ステータ5,14及び第1、第2ロータ7,23は、垂直配列の場合に限らず、水平配列としてもよい。この場合、第2ステータ14は、支軸22を中心と回動可能としてもよく、あるいは、第1ステータ5の軸線の延長上において第1ステータ5に対して相対的に接近離隔可能としてもよい。
更に、供給、排出ケーシング4,18の原料供給口3、製品排出口17は、接線方向に設ける場合に限らず、半径方向に設けてもよい。
【0034】
【発明の効果】
以上説明したように、本発明の微粉砕機によれば、第1、第2ロータの回転数(周速)を個別に設定可能となるので、原料の特性の変化に対応させて所望の特性の製品を得ることができる。
【0035】
一方、第1、第2ステータが分離可能であることにより、それぞれのステータ及びロータの清掃が可能となるので、種類の異なる原料の処理にも容易に対応することができる。
【0036】
第1、第2ロータの少なくとも一方が可逆回転可能であることにより、第1、第2ロータの回転方向が同一又は互いに逆となり、同一の場合、被粉砕物が第1ロータと第1ステータによる粉砕室から第2ロータと第2ステータによる粉砕室へ移動する際の速度変化が少なくなるので、消費動力の少ない運転を行うことができる一方、互いに逆の場合、被粉砕物が第1ロータと第1ステータによる粉砕室から第2ロータと第2ステータによる粉砕室へ移動する際の速度変化が大きくなって、衝撃力が大きくなるので、より細かな粉砕を行うことができる。
又、ロータとステータの凹部及び凸部の横断面形状がそれぞれの母線に対して対称な方形状で、ロータの回転方向の違いにより粉砕性能が変化しない場合、ステータ及びロータの摩耗が均等になるので、耐用寿命を長くすることができる。
【0037】
第1、第2ロータの少なくとも一方が反転可能であることにより、ロータとステータの凹部及び凸部の横断面形状がそれぞれの母線に対して非対称な三角形状である場合、ロータの回転方向の変更に対応可能となるので、粉砕性能の低下を招くことがない。
【0038】
又、第1、第2ステータの少なくとも一方が反転可能であることにより、ロータとステータの凹部及び凸部の横断面形状がそれぞれの母線に対して非対称な三角形状である場合、ロータの回転方向の変更に対応可能となるので、粉砕性能の低下を招くことがない。
【図面の簡単な説明】
【図1】本発明に係る微粉砕機の実施の形態の一例を示す一部を破断した側面図である。
【図2】図1の微粉砕機における第1ステータと第2ステータを分離した状態の側面図である。
【符号の説明】
1 第1ベースプレート
3 原料供給口
4 供給ケーシング
5 第1ステータ
7 第1ロータ
7a 凹部と凸部
13 ステータ押え
14 第2ステータ
15 クランプ手段
17 製品排出口
18 排出ケーシング
19 第2ベースプレート
21 分離用ポスト
22 支軸
23 第2ロータ
23a 凹部と凸部
M 原料
P 製品
[0001]
TECHNICAL FIELD OF THE INVENTION
The present invention relates to a fine pulverizer for finely pulverizing raw materials (substances to be pulverized) such as resin mixtures such as resins and toners, chemical products, minerals, metals, foods and chemicals into fine particles of 5 to 100 microns. In particular, it relates to a pulverizer having a two-stage rotor.
[0002]
[Prior art]
Conventionally, this type of fine pulverizer includes two types of pulverizing units, a first pulverizing unit including a pulverizer and a stator opposed thereto and a second pulverizing unit including a rotor and a stator opposed thereto. Are arranged coaxially in the vertical and vertical directions, and a radial crusher is provided on the outer periphery of the rotor of the first crushing section with a certain gap between the rotator and the stator opposed thereto. A protruding portion is formed on the outer periphery of the rotor at a certain gap between the rotor and the opposing stator, and a protruding portion is formed on the surface of the bus bar. A device provided with an outlet is disclosed (for example, see Patent Document 1).
[0003]
[Patent Document 1]
Japanese Patent Publication No. Sho 59-19739
According to the above-mentioned fine pulverizer, a relatively large lump is pulverized in advance in the first pulverizing section, and fine particles are pulverized finely in the second pulverizing section. Properties can be significantly improved. At the same time, it is possible to save a great deal of labor of previously grinding the material to be ground to an appropriate particle size.
[0005]
Further, a rotor supported by the rotating shaft and having a concave portion and a convex portion parallel to the bus line alternately continuous in the circumferential direction on the outer surface, and a rotor fitted on the inner surface with a minute gap fitted outside the rotor with a small gap therebetween. In a fine pulverizer for finely pulverizing the raw material between a stator and a concave part and a convex part which are alternately arranged in the circumferential direction in parallel with the rotor, the rotor is divided into two or more stages, and from the lowermost stage on the raw material supply port side. There is also disclosed one in which the numbers of concave portions and convex portions are sequentially increased toward the uppermost stage on the product discharge port side (for example, see Patent Document 2).
[0006]
[Patent Document 2]
JP 2000-5614 A
According to the above-mentioned pulverizer, the raw material sucked together with air into the pulverizing chamber between the rotor and the stator gradually decreases in particle size as the pulverization progresses, and the pulverized product exiting the pulverizing chamber has a micron size. The particles have a very narrow particle size distribution width on the order, and the average particle size becomes extremely small.
[0008]
Furthermore, a rotor provided on the rotating shaft and having a concave portion and a convex portion parallel to the generatrix on the outer peripheral surface alternately and continuously provided in the circumferential direction is divided into a plurality of stages, and the outer diameter is sequentially increased from the lower stage to the upper stage. Increase the number of concaves and convexes and increase the number of concaves and convexes, and the concaves and convexes parallel to the generating line are alternately and continuously fitted on the inner peripheral surface of the rotor with a small gap therebetween. The provided stator is divided into a plurality of stages, and the inner diameter is sequentially increased from the lower stage to the upper stage, and the number of the concave portions and the convex portions is increased, and the space between the rotor and the stator is sucked together with air. It is also known that the raw material is finely pulverized by high-speed rotation of the rotor (for example, see Patent Document 3).
[0009]
JP 2000-15123 A
According to the above-mentioned pulverizer, even if the number of the unevenness of the rotor and the unevenness of the stator is increased in the upper stage, the outer diameter of the rotor, the inner diameter of the stator is increased in the upper stage, and the rotor and the stator are Since the micro-gap of the crushing chamber is almost constant, the cross-sectional area of the crushing chamber does not decrease, the flow velocity in the crushing chamber can be almost constant, or slightly reduced, and the passage time of the particles is almost constant in each part, or The length of the crushing chamber is longer at the upper portion, and the crushing process is sufficiently performed. Moreover, since the pressure loss of the airflow is small, it is not necessary to increase the size of the suction blower. Further, since the outer diameter of the rotor on the outlet side of the pulverizing chamber is large, the peripheral speed of the rotor is increased, which is effective for further pulverizing the fine particles.
[0011]
[Problems to be solved by the invention]
However, in any of the conventional pulverizers, since the two-stage rotor is supported on the same rotating shaft, the number of rotations of the rotor in each stage becomes the same, and by changing the rotor diameter in both stages, Can be changed, but the ratio of the peripheral speeds of both is kept constant.
Therefore, for example, when an attempt is made to obtain a pulverized product (product) having a required particle size, the number of rotations of the rotor is specified to one according to the characteristics of the raw material, that is, the grindability (easiness of pulverization) and the particle size. The particle size distribution and production amount of the product are also determined by the determined rotation speed.
However, the effective peripheral speed of the rotor in each stage varies depending on the characteristics of the raw material and the required characteristics of the product (particle size, particle size distribution, particle shape, etc.) and is not uniform.
[0012]
Therefore, an object of the present invention is to provide a fine pulverizer capable of obtaining a product having desired characteristics in response to a change in the characteristics of a raw material.
[0013]
[Means for Solving the Problems]
In order to solve the above problem, a fine pulverizer of the present invention is provided with a short cylindrical supply casing having one end closed and a raw material supply port provided on a peripheral wall, and is connected to the other end of the supply casing via one end. A first stator having a cylindrical shape in which concave portions and convex portions parallel to the bus are alternately continuous in the circumferential direction on the inner surface; a first stator is inserted inside the first stator with a small gap therebetween; And a concave portion and a convex portion which are parallel to each other are alternately continuous in the circumferential direction, and have a cylindrical shape with both ends closed. The first rotor having a variable number of rotations is connected to the other end of the first stator via one end, and has an inner surface. A second stator having a cylindrical shape in which concave portions and convex portions parallel to the bus bar are alternately arranged in the circumferential direction in the circumferential direction; a second stator is inserted inside the second stator with a small gap therebetween; It has a cylindrical shape with both ends closed, with concave and convex portions parallel to A second rotor having a variable number of rotations, and a discharge casing having a short cylindrical shape, which is connected to the other end of the second stator via one end, has the other end closed, and has a product discharge port on the peripheral wall. It is characterized by.
[0014]
On the other hand, the first and second stators are preferably separable.
Preferably, at least one of the first and second rotors is capable of reversible rotation.
It is preferable that at least one of the first and second rotors is reversible.
Preferably, at least one of the first and second stators is reversible.
[0015]
[Action]
In the pulverizer of the present invention, the rotation speeds (peripheral speeds) of the first and second rotors can be individually set.
[0016]
The arrangement of the first and second stators and the first and second rotors may be either vertical or horizontal.
[0017]
The fine gap (pulverization chamber) between the first stator and the first rotor and between the second stator and the second rotor is preferably 5 mm or less. For example, when obtaining fine powder having a particle size of 5 to 20 μm, about 1 mm is preferable. desirable.
The minute gaps between the first stator and the first rotor and between the second stator and the second rotor may be the same or different. For example, when finely pulverizing a raw material having a large particle size, the fine gap between the first stator and the first rotor is preferably larger than the fine gap between the second stator and the second rotor.
[0018]
The outer diameters of the first rotor and the second rotor may be the same or different. For example, when obtaining fine powder having a particle size of 5 to 20 μm, the outer diameter of the second rotor is preferably larger than the outer diameter of the first rotor.
[0019]
The cross-sectional shapes of the concave and convex portions of the first and second stators and the first and second rotors are determined by the characteristics of the raw material and the required characteristics of the product. Combinations are preferred, and their depth is about 1-5 mm. For example, in the case of a coarse (square) raw material, the concave and convex portions of the first stator and the first rotor are preferably a combination of triangular cross sections.
The numbers of the concave portions and the convex portions of the first stator, the first rotor, the second stator, and the second rotor may be the same or different. For example, when obtaining fine powder having a particle size of 5 to 20 μm, the number of the concave portions and the convex portions of the second stator and the second rotor is preferably larger than the number of the concave portions and the convex portions of the first stator and the first rotor.
[0020]
On the other hand, since the first stator and the second stator are separable, each of the stator and the rotor can be cleaned.
[0021]
It is preferable that the supply casing and the first stator, the first rotor and the rotation shaft, and the like, the second stator and the discharge casing, the second rotor and the rotation shaft, and the like can also be separated from each other. Can be easily and reliably performed.
[0022]
Since at least one of the first and second rotors is capable of reversible rotation, the rotation directions of the first and second rotors are the same or opposite to each other. The speed change (acceleration) when moving from the crushing chamber to the crushing chamber by the second rotor and the second stator is reduced, while when the speed is opposite to each other, the object to be crushed is moved from the crushing chamber by the first rotor and the first stator to the second. The speed change when moving to the grinding chamber by the rotor and the second stator increases, and the impact force increases.
Further, when the cross-sectional shapes of the concave and convex portions of the rotor and the stator are symmetrical with respect to the respective generatrix and the crushing performance does not change due to the difference in the rotation direction of the rotor, the wear of the stator and the rotor becomes uniform. .
[0023]
Since at least one of the first and second rotors is reversible, when the transverse cross-sectional shape of the concave portion and the convex portion of the rotor and the stator is asymmetrical triangular with respect to the respective generatrix, the rotation direction of the rotor is changed. Can be supported.
[0024]
Further, since at least one of the first and second stators is reversible, when the transverse cross-sectional shape of the concave portion and the convex portion of the rotor and the stator is a triangular shape that is asymmetric with respect to the respective generatrix, the rotational direction of the rotor is Can be changed.
[0025]
In addition, it is preferable that at least one of the supply and discharge casings is reversible, so that when the respective material supply ports and product discharge ports are provided in a tangential direction, the rotation direction of the rotor is changed. Can be supported.
[0026]
BEST MODE FOR CARRYING OUT THE INVENTION
Hereinafter, embodiments of the present invention will be described with reference to the drawings.
FIG. 1 is a partially cutaway side view showing an example of an embodiment of a pulverizer according to the present invention.
[0027]
In FIG. 1, reference numeral 1 denotes a first base plate horizontally mounted on a gantry 2 to serve as a lid and a positioning member of a supply casing to be described later, on which the raw material M is supplied to the peripheral wall from the tangential direction. A supply casing 4 having a short cylindrical shape with flanges at both ends provided with a raw material supply port 3 for reversing (in FIG. 1, repeated up and down) is brought into contact with a flange at one end (lower end in FIG. 1). , Are positioned and mounted.
At the other end (upper end in FIG. 1) of the supply casing 4, concave portions and convex portions (not shown) parallel to the generatrix are alternately continuous in the circumferential direction on the inner surface of the peripheral wall having the same outer diameter as the inner diameter. A first stator 5 having a cylindrical shape with flanges at both ends, which can be inverted (in FIG. 1, repeatedly flipped up and down), has one end inserted into the other end of the supply casing 4 and one end flange connected to the other end of the supply casing 4. The first stator 5 is provided with a cooling jacket 6 for cooling the first stator 5 outside the peripheral wall of the first stator 5 by being brought into contact with the flange at the end to be positioned coaxially.
The inside of the first stator 5 has a cylindrical shape with both ends closed in which concave portions and convex portions 7a parallel to the generatrix are alternately continuous on the outer surface in the circumferential direction, and can be turned over (inverted up and down in FIG. 1). And a first rotor 7 having a length substantially equal to that of the first stator 5 is inserted with a small gap (pulverizing chamber) (not shown). The bearing is inserted through a bearing (not shown) into a cylindrical bearing housing 8 inserted into the first base plate 1 so as to be positioned at the axial center of the first base plate 1, and projects from the bearing housing 8 into the first stator 5. The shaft 9 is detachably supported at the end of the rotating shaft 9 via a substantially axially intermediate portion of the shaft center.
The rotating shaft 9 has a pulley (not shown) provided at an end protruding from the bearing housing 8 toward the gantry 2, and a variable rotation speed and reversible rotation mounted on the gantry 2 via an L-shaped bracket 10. The belt 12 is wrapped around a pulley (not shown) provided on the output shaft 11a of the first motor 11, which is linked to the first motor.
[0028]
Also, on the first base plate 1, two stator holding posts (not shown) are erected at point symmetrical positions about the axis of the supply casing 4, and on both posts, A substantially annular plate-shaped stator retainer 13 which is fitted to the other end of the first stator 5 and abuts on the flange at the other end presses the first stator 5 and the supply casing 4 against the first base plate 1 and presses them. It is bolted to maintain the airtightness of the connection part.
[0029]
At the other end of the first stator 5, a concave portion and a convex portion (not shown) are formed on the inner surface of the peripheral wall having an inner diameter slightly larger than the inner diameter and shorter than the first stator 5 and parallel to the generating line. ) Are alternately continuous in the circumferential direction, and the second stator 14 which can be inverted (in FIG. 1, repeatedly flipped up and down) abuts the flange at one end thereof with the stator presser 13, and By being connected to the stator presser 13 by a plurality of clamping means 15 such as bolts and nuts, it is coaxially positioned and airtightly connected to the first stator 5, and is provided outside the peripheral wall of the second stator 14. Similarly to the first stator 5, a cooling jacket 16 for cooling the second stator 14 is provided.
The other end of the second stator 14 has a short cylindrical shape with flanges at both ends provided with a product discharge port 17 for discharging the product P in a tangential direction on a peripheral wall having the same inner diameter as the outer diameter thereof. The discharge casing 18 which can be repeatedly turned upside down is coaxially positioned by fitting one end to the other end of the second stator 14 and abutting one end flange to the other end flange of the second stator 14. It is placed.
It should be noted that a suction blower (not shown) and the like are connected to the product discharge port 17.
At the other end of the discharge casing 18, a second base plate 19 also serving as a lid thereof is positioned and mounted by abutting on a flange at the other end of the discharge casing 18. A plurality of fasteners 20 such as bolts and nuts are used to press the second stator 14 and the discharge casing 18 against the second base plate 19 to maintain the airtightness of the connection between the second stator 14 and the discharge casing 18. While being fastened, it is pivotally supported on the upper end of a portal-shaped separation post 21 erected on the gantry 2 by a horizontal support shaft 22, and about 90 ° from a horizontal state to a vertical state around the support shaft 22. (See FIG. 2).
The inside of the second stator 14 has a cylindrical shape with both ends closed in which concave portions and convex portions 23a parallel to the generatrix are alternately continuous in the circumferential direction on the outer surface, and is inverted (in FIG. 1, repeatedly up and down). A second rotor 23 that is possible and has a length substantially equal to that of the second stator 14 is inserted with a minute gap (pulverization chamber) (not shown). A bearing (not shown) is inserted through a cylindrical bearing housing 24 inserted into the second base plate 19 so as to be positioned at the axial center of the bearing 18, and is inserted into the second stator 14 from the bearing housing 24. An end of a protruding rotating shaft (not shown) is supported so as to be separable through a substantially middle portion of the shaft center in the circumferential direction.
The rotating shaft is connected to a pulley (not shown) provided at an end protruding from the bearing housing 24 to the opposite side (upward in FIG. 1) of the second stator 14 and a support shaft 22 side of the second base plate 19. By rotating a belt (both not shown) around a pulley provided on an output shaft 26a of a second motor 26 capable of variable rotation and reversible rotation mounted via a T-shaped bracket 25, the second motor 26 and is interlockingly connected.
In FIG. 1, reference numeral 27 denotes a second base plate rotation preventing member provided on the T-shaped bracket 25 so as to surround the second motor 26, and abuts against a stopper 28 provided on the separation post 21 to rotate the second base plate 19. 29 is a cover that covers the pulley of the second motor 26, the pulley of the rotating shaft, the belt, and the like.
[0030]
In the pulverizer having the above structure, when the suction blower and the first and second motors 11 and 26 are operated, the raw material M is supplied together with the gas into the supply casing 4 and the first rotor 7 is rotated at a high speed. After being crushed by impact, collision, and grinding action in the minute gap between the first rotor 5 and the second stator 23, the second rotor 23 and the second stator 14 are rotated at high speed separately from the first rotor 7. The particles P are finely pulverized by a striking, collision, attrition, and particle size adjusting action in the small gap therebetween, reach the discharge casing 18, and the product P is discharged out of the machine together with the gas.
[0031]
In the above-mentioned pulverizer, when the coarse raw material M is finely pulverized, the concave portion and the convex portion 7a of the first stator 5 and the first rotor 7 have a triangular cross section, and the concave portions of the second stator 14 and the second rotor 23 have the same shape. The number of the protrusions 23a may be larger than the number of the recesses and the protrusions 7a of the first stator 5 and the first rotor 7, or the inner diameter of the second stator 14 and the outer diameter of the second rotor 23 may be equal to the inner diameter of the first stator 5, The outer diameter of the first rotor 7 is made larger, or the rotation speed of the second rotor 23 is made larger than the rotation speed of the first rotor.
Further, when adjusting the production amount, the grain shape, the width of the particle size distribution, etc. of the product P, the rotation speeds (peripheral speeds) of the first rotor 7 and the second rotor 23 are appropriately combined according to the characteristics of the raw material M.
Furthermore, when the operation with less power consumption is performed, the rotation directions of the first and second rotors 7 and 23 are made the same, while when a finer product P is obtained, the rotation direction of the first and second rotors 7 and 23 is changed. Reverse each other.
Furthermore, in order to prevent uneven wear of the first and second stators 5 and 14 and the first and second rotors 7 and 23, the first and second stators 5 and 14 and the first and second rotors 7 and 23 are required. Then, the supply and discharge casings 4 and 18 are appropriately inverted, and the first and second rotors 7 and 23 are appropriately rotated forward or reverse.
[0032]
On the other hand, when cleaning the inside by changing the type of the raw material M, first, the connection between the second stator 14 and the stator presser 13 by the clamp means 15 is released, and as shown in FIG. Is rotated about the support shaft 22 to separate the first stator 5 and the second stator 14.
Next, the pressing of the first stator 5 and the supply casing 4 by the stator retainer 13 is released, and the first rotor 7 is detached from the rotating shaft 9, so that the first stator 5, the first rotor 7, the supply casing 4, etc. Can be individually cleaned.
Further, by releasing the fastening between the second stator 14 and the second base plate 19 by the fastener 20 and removing the second rotor 23 from the rotating shaft, the second stator 14, the second rotor 23, the discharge casing 18, etc. Individual cleaning becomes possible.
[0033]
In the above-described embodiment, the case where the driving of the first and second rotors 7 and 23 transmits the rotation of the first and second motors 11 and 26 via the transmission means has been described. The present invention is not limited to this, and may be directly performed by a built-in motor in which a motor rotor is directly incorporated in a rotating shaft.
Further, the first and second stators 5 and 14 and the first and second rotors 7 and 23 are not limited to a vertical arrangement, but may be a horizontal arrangement. In this case, the second stator 14 may be rotatable about the support shaft 22, or may be relatively close to and away from the first stator 5 along an extension of the axis of the first stator 5. .
Further, the raw material supply port 3 and the product discharge port 17 of the supply / discharge casings 4 and 18 are not limited to being provided in the tangential direction, but may be provided in the radial direction.
[0034]
【The invention's effect】
As described above, according to the pulverizer of the present invention, the rotation speeds (peripheral speeds) of the first and second rotors can be individually set, so that the desired characteristics can be adjusted according to the change in the characteristics of the raw material. Products can be obtained.
[0035]
On the other hand, since the first and second stators can be separated, the respective stators and rotors can be cleaned, so that it is possible to easily cope with the processing of different types of raw materials.
[0036]
Since at least one of the first and second rotors is capable of reversible rotation, the rotation directions of the first and second rotors are the same or opposite to each other. Since the speed change when moving from the crushing chamber to the crushing chamber by the second rotor and the second stator is reduced, the operation with less power consumption can be performed. The speed change when moving from the first stator crushing chamber to the second rotor and the second stator crushing chamber becomes large and the impact force becomes large, so that finer crushing can be performed.
Further, when the cross-sectional shapes of the concave and convex portions of the rotor and the stator are symmetrical with respect to the respective generatrix and the crushing performance does not change due to the difference in the rotation direction of the rotor, the wear of the stator and the rotor becomes uniform. Therefore, the service life can be extended.
[0037]
Since at least one of the first and second rotors is reversible, when the transverse cross-sectional shape of the concave portion and the convex portion of the rotor and the stator is asymmetrical triangular with respect to the respective generatrix, the rotation direction of the rotor is changed. Therefore, a reduction in crushing performance does not occur.
[0038]
Further, since at least one of the first and second stators is reversible, when the transverse cross-sectional shape of the concave portion and the convex portion of the rotor and the stator is a triangular shape that is asymmetric with respect to the respective generatrix, the rotational direction of the rotor is Therefore, it is possible to cope with the change in crushing performance, so that the crushing performance is not reduced.
[Brief description of the drawings]
FIG. 1 is a partially cutaway side view showing an example of an embodiment of a pulverizer according to the present invention.
FIG. 2 is a side view of the pulverizer of FIG. 1 in a state where a first stator and a second stator are separated.
[Explanation of symbols]
DESCRIPTION OF SYMBOLS 1 1st base plate 3 raw material supply port 4 supply casing 5 1st stator 7 1st rotor 7a recessed part and convex part 13 stator holding 14 second stator 15 clamping means 17 product discharge port 18 discharge casing 19 second base plate 21 separation post 22 Support shaft 23 Second rotor 23a Concave and convex portions M Raw material P Product

Claims (5)

一端を閉止しかつ周壁に原料供給口を設けた短円筒状を呈する供給ケーシングと、供給ケーシングの他端に一端を介して連設され、内側表面に母線と平行な凹部と凸部を交互に周方向へ連続させた円筒状を呈する第1ステータと、第1ステータの内側に微小間隙を存して嵌挿され、外側表面に母線と平行な凹部と凸部を交互に周方向へ連続させた両端閉止の円筒状を呈し、回転数可変の第1ロータと、第1ステータの他端に一端を介して連設され、内側表面に母線と平行な凹部と凸部を交互に周方向へ周方向へ連続させた円筒状を呈する第2ステータと、第2ステータの内側に微小間隙を存して嵌挿され、外側表面に母線と平行な凹部と凸部を交互に周方向へ連続させた両端閉止の円筒状を呈し、回転数可変の第2ロータと、第2ステータの他端に一端を介して連設され、他端を閉止しかつ周壁に製品排出口を設けた短円筒状の排出ケーシングとを備えることを特徴とする微粉砕機。A supply casing having a short cylindrical shape, one end of which is closed and a raw material supply port is provided on the peripheral wall, and a concave part and a convex part which are connected to the other end of the supply casing via one end and which are parallel to the generating line are alternately provided on the inner surface. A first stator having a cylindrical shape continuous in the circumferential direction, and a concave portion and a convex portion parallel to the generating line are alternately connected in the circumferential direction to be inserted inside the first stator with a small gap therebetween, and to be continuous in the circumferential direction. It has a cylindrical shape with both ends closed, and has a variable number of revolutions, a first rotor, and a concavity and a convex portion, which are connected to the other end of the first stator via one end and are parallel to the generatrix on the inner surface, in the circumferential direction. A second stator having a cylindrical shape that is continuous in the circumferential direction, and a concave portion and a convex portion that are inserted inside the second stator with a small gap therebetween and that are parallel to the generating line on the outer surface are alternately continuous in the circumferential direction. A second rotor having a cylindrical shape with both ends closed and having a variable number of revolutions, and a second stator It is continuously provided via one end to the end, mill, characterized in that it comprises a short cylindrical discharge casing provided with a product discharge port at the other end to the closure and and the peripheral wall. 前記第1、第2ステータが分離可能であることを特徴とする請求項1記載の微粉砕機。The pulverizer according to claim 1, wherein the first and second stators are separable. 前記第1、第2ロータの少なくとも一方が可逆回転可能であることを特徴とする請求項1又は2記載の微粉砕機。The pulverizer according to claim 1 or 2, wherein at least one of the first and second rotors is capable of reversible rotation. 前記第1、第2ロータの少なくとも一方が反転可能であることを特徴とする請求項1、2又は3記載の微粉砕機。4. The pulverizer according to claim 1, wherein at least one of the first and second rotors is reversible. 前記第1、第2ステータの少なくとも一方が反転可能であることを特徴とする請求項1、2、3又は4記載の微粉砕機。5. The pulverizer according to claim 1, wherein at least one of the first and second stators is reversible.
JP2003128740A 2003-05-07 2003-05-07 Pulverizer Expired - Fee Related JP3832831B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2003128740A JP3832831B2 (en) 2003-05-07 2003-05-07 Pulverizer

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2003128740A JP3832831B2 (en) 2003-05-07 2003-05-07 Pulverizer

Related Child Applications (1)

Application Number Title Priority Date Filing Date
JP2006162485A Division JP4265807B2 (en) 2006-06-12 2006-06-12 Pulverizer

Publications (2)

Publication Number Publication Date
JP2004330062A true JP2004330062A (en) 2004-11-25
JP3832831B2 JP3832831B2 (en) 2006-10-11

Family

ID=33504771

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2003128740A Expired - Fee Related JP3832831B2 (en) 2003-05-07 2003-05-07 Pulverizer

Country Status (1)

Country Link
JP (1) JP3832831B2 (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2008012477A (en) * 2006-07-07 2008-01-24 Furukawa Industrial Machinery Systems Co Ltd Pneumatic pulverizer and method for recovering residue in its casing
EP2103996A1 (en) 2008-03-17 2009-09-23 Ricoh Company, Ltd. Method for preparing toner, toner prepared by the method, and image forming apparatus using the toner
JP2013086032A (en) * 2011-10-18 2013-05-13 Sugino Machine Ltd Pulverizer
EP2705907A2 (en) 2012-09-07 2014-03-12 Ricoh Company, Ltd. Toner producing apparatus and toner producing method
CN105471136A (en) * 2016-01-06 2016-04-06 常州市龙鑫化工机械有限公司 Rotor assembly capable of rotor replacement and grinding machine provided with rotor assembly
CN115888927A (en) * 2022-12-29 2023-04-04 浙江迦南科技股份有限公司 Granule finishing knife convenient to install

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2008012477A (en) * 2006-07-07 2008-01-24 Furukawa Industrial Machinery Systems Co Ltd Pneumatic pulverizer and method for recovering residue in its casing
EP2103996A1 (en) 2008-03-17 2009-09-23 Ricoh Company, Ltd. Method for preparing toner, toner prepared by the method, and image forming apparatus using the toner
US8257900B2 (en) 2008-03-17 2012-09-04 Ricoh Company, Limited Method for preparing toner, toner prepared by the method, and image forming apparatus using the toner
JP2013086032A (en) * 2011-10-18 2013-05-13 Sugino Machine Ltd Pulverizer
EP2705907A2 (en) 2012-09-07 2014-03-12 Ricoh Company, Ltd. Toner producing apparatus and toner producing method
CN105471136A (en) * 2016-01-06 2016-04-06 常州市龙鑫化工机械有限公司 Rotor assembly capable of rotor replacement and grinding machine provided with rotor assembly
CN115888927A (en) * 2022-12-29 2023-04-04 浙江迦南科技股份有限公司 Granule finishing knife convenient to install
CN115888927B (en) * 2022-12-29 2024-05-14 浙江迦南科技股份有限公司 Whole grain sword convenient to installation

Also Published As

Publication number Publication date
JP3832831B2 (en) 2006-10-11

Similar Documents

Publication Publication Date Title
JP5730761B2 (en) Conical impact mill
CN101664709A (en) Crushing equipment
JP2010540238A (en) Roller mill and raw material pulverization method using the same.
JP4265807B2 (en) Pulverizer
JP2003236399A (en) Impact crushing apparatus for grain
JP2004330062A (en) Pulverizer
JP3273394B2 (en) Mechanical grinding equipment
JP2000271503A (en) Method for operating vertical crusher
JP2006167515A (en) Pulverizer
JP2003181316A (en) Medium agitation and crushing device and crushing treatment system having the device
US11007531B2 (en) Adjustable super fine crusher
JP3821651B2 (en) Waste supply device
JP2905196B1 (en) Pulverizer
JP3725330B2 (en) Crusher
JP4288649B2 (en) Vertical crusher
JP2002239403A (en) Grinder
JP3147143B2 (en) Vertical crusher
JP2884515B1 (en) Fine grinding equipment
JPH07213940A (en) Grinder
EP1506815B1 (en) Impact grinding apparatus for cereal
KR200385083Y1 (en) A Device of Wet Milling Machine for Separating and Discharging Fine Grained Powder
JP2002320868A (en) Vertical crusher
JP2004122070A (en) Vertical grinding mill
JPH0474542A (en) Vertical mill
JP2001340781A (en) Fine grinding machine

Legal Events

Date Code Title Description
RD02 Notification of acceptance of power of attorney

Effective date: 20041224

Free format text: JAPANESE INTERMEDIATE CODE: A7422

RD04 Notification of resignation of power of attorney

Effective date: 20041228

Free format text: JAPANESE INTERMEDIATE CODE: A7424

A521 Written amendment

Free format text: JAPANESE INTERMEDIATE CODE: A821

Effective date: 20041224

A711 Notification of change in applicant

Free format text: JAPANESE INTERMEDIATE CODE: A712

Effective date: 20050927

A977 Report on retrieval

Free format text: JAPANESE INTERMEDIATE CODE: A971007

Effective date: 20051012

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20051109

A521 Written amendment

Effective date: 20060110

Free format text: JAPANESE INTERMEDIATE CODE: A523

A02 Decision of refusal

Effective date: 20060412

Free format text: JAPANESE INTERMEDIATE CODE: A02

A521 Written amendment

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20060612

A911 Transfer of reconsideration by examiner before appeal (zenchi)

Effective date: 20060616

Free format text: JAPANESE INTERMEDIATE CODE: A911

TRDD Decision of grant or rejection written
A01 Written decision to grant a patent or to grant a registration (utility model)

Effective date: 20060712

Free format text: JAPANESE INTERMEDIATE CODE: A01

A61 First payment of annual fees (during grant procedure)

Effective date: 20060714

Free format text: JAPANESE INTERMEDIATE CODE: A61

R150 Certificate of patent (=grant) or registration of utility model

Free format text: JAPANESE INTERMEDIATE CODE: R150

FPAY Renewal fee payment (prs date is renewal date of database)

Year of fee payment: 3

Free format text: PAYMENT UNTIL: 20090728

S531 Written request for registration of change of domicile

Free format text: JAPANESE INTERMEDIATE CODE: R313531

FPAY Renewal fee payment (prs date is renewal date of database)

Free format text: PAYMENT UNTIL: 20090728

Year of fee payment: 3

R350 Written notification of registration of transfer

Free format text: JAPANESE INTERMEDIATE CODE: R350

LAPS Cancellation because of no payment of annual fees